Inorganic ion sorbent method

ABSTRACT

A process and medium for decontamination of water containing anionic species including arsenic and chromium, wherein compounds comprising divalent and trivalent metal oxides and sulfides are used to form surface complexes with contaminants under pH conditions within the range of potable water. In one embodiment natural and synthetic spinels and spinel-like materials are used as the sorbent substance.

This application is a continuation of prior application Ser. No. 09/886,175 filed Jun. 20, 2001 which is hereby incorporated herein by reference.

This invention was made with support from the United States Government under Contract DE-AC04-96AL85000 awarded by the US Department of Energy. The Government has certain rights in this invention.

BACKGROUND OF THE INVENTION

1. Field of the Invention

This invention pertains to decontamination of fluids containing ionic contaminants, especially water containing anionic contaminants. In particular, the invention relates to the removal of arsenic contaminants and chromate from water by treating the water using adsorbent compounds comprised of divalent and trivalent metal oxides and sulfides.

2. Description of the Related Art

For purposes of this disclosure, unless otherwise specified, the term “metal oxides” is intended to include both metal oxides and metal hydroxides. Likewise, the term “metal sulfides” is intended to include both metal sulfides and metal hydrosulfides. Similarly, for purposes of this disclosure, “arsenic contaminants” includes both arsenates and arsenites.

Arsenic contaminants are examples of anionic contaminants that may be present in water as a result of natural as well as human-mediated causes. The long-term availability of safe and affordable drinking water depends, in part, on availability of effective and economical treatment means for removing arsenic contaminants (as well as other anionic contaminants including chromate) from water. Successful treatment strategies, in turn, depend on not otherwise significantly altering the water characteristics (for example, its pH) in ways that would make it non-potable.

Arsenic and other anionic contaminants likewise pose risks when present in fluids other than drinking water sources. For example, waste water streams often contain such contaminants and require remediation even where they are not considered to be directly associated with potable drinking water sources.

Various sorbent methods for removing arsenic contaminants and other anionic contaminants from water have been used and developed previously. For example, certain trivalent metal hydroxide compounds, such as Al₂O₃ and Fe₂O₃, have been demonstrated to sorb anionic contaminants, including arsenic contaminants, from water. A drawback associated with use of such trivalent compounds alone is that, because they typically exhibit a point of zero charge from pH 7 to 9, the water to be treated may need to be acidified in order for these compounds to sorb anions to a significant degree. Thus, after treatment, in order to restore the potability of the treated water, further amendments must be added to bring the pH back up to a safely drinkable range. Similarly, tetravalent metal oxides such as SiO₂ could be effective anion sorbents, however, their point of zero charge is typically around pH 2, so extremely acidic conditions would needed for tetravalent metal oxides to sorb anions. Additionally, these substances are considered likely to fall outside of the range of useful sorbents because of other chemical issues associated with operating at such low pH.

The divalent oxide MgO, likewise, has been shown chemically to sorb anions including arsenic in water. Although use of MgO does not necessitate driving the pH of water outside of the potable range (divalent metal oxides tend to exhibit a point of zero charge that is pH 10 or higher), the effectiveness of MgO as a sorbent for water decontamination, however, can be limited. This is due to its tendency to form carbonates in the presence of carbon in the water from natural (e.g. biological and atmospheric) sources. When this occurs, the carbonate species formed at the surface lack any significant electrostatic attraction for negatively-charged ions. Thus, the sorbency of the MgO can be short-lived absent taking steps to reverse of the carbonate reaction and restore the sorbent.

The sorbency methods just discussed rely on the electrostatic attraction between positively charged surface species and negatively charged contaminants. An altogether different mechanism that has been exploited to decontaminate water containing ionic contaminant species is ion exchange. Examples of ion exchange materials suitable for water decontamination include hydrotalcites (which exchange anions) and zeolites (which exchange cations). Although ion exchange materials have been shown to be effective without causing the types of problems associated with Fe(OH)₃ and Al₂O₃ (pH concerns) or MgO (carbonate issues), ion exchange materials can be very expensive. Zeolites that allow for separations based on size are also used in some decontamination applications, but they do not sorb anionic species such as chromate and arsenic contaminants in water.

Therefore, the need remains for improved liquid decontamination approaches that are inexpensive, yet effective in removing anionic contaminants, including chromate, arsenates and arsenites.

SUMMARY OF THE INVENTION

In one aspect, the invention provides a water decontamination process comprising contacting water containing anionic contaminants with sorbent material that binds anionic species predominantly through the formation of surface complexes, wherein the sorbent material comprises divalent metals and trivalent metals.

In another aspect, the invention provides a decontamination medium for water comprising sorbent material that binds anionic species predominantly through the formation of surface complexes, wherein the sorbent material comprises divalent metals and trivalent metals.

DETAILED DESCRIPTION OF THE INVENTION

This invention utilizes the principle that metal oxides and metal sulfides, at pH below their point of zero charge, attract negatively charged species. This is due to a phenomenon wherein, at pH below the point of zero charge for a given metal oxide or metal sulfide, surface metal groups tend to be more fully protonated (and thus more likely to exhibit a positive charge) than at pH at or above the point of zero charge. As a result, at pH below the point of zero charge, negatively-charged species can be removed from solution through the formation of ion-bearing surface complexes with the metal oxide or metal sulfide surface groups.

The mixed divalent and trivalent metal oxide and metal sulfide materials employed in the present invention to adsorb negatively-charged contaminant species in water do so at pH within the drinkable range for water. Moreover, the materials tested do not exhibit the tendency to form carbonates to a degree sufficient to render them inactive for purposes of anion sorption. According to the invention, sorbent materials effective for sequestering arsenic-containing contaminants from water are selected, or can be engineered, to exhibit a point of zero charge that permits anion sorption in the pH range of potable water.

An example of mixed valency inorganic materials capable of sorbing anions such as arsenic contaminants and chromate in water is found in natural and synthetic spinels and inverse spinels, as well as “spinel-like” materials. These inorganic materials are generally characterized by the chemical formula (AB₂X₄)_(n) where A and B represent cations of differing valencies (such as A=Mg²⁺ and B=Al³⁺) and X represents one or more anions (such as O²⁻ or S²⁻) and n is at least 1. (For purposes of this disclosure, these stoichiometries are intended to be approximate so that where the formula (AB₂X₄)_(n) is used in this disclosure, this means that B has a prevalence of about twice that of A and X has a prevalence of about four times that of A. Also, in this disclosure, “spinel-like” is intended to encompass substances generally exhibiting the stoichiometry just noted, but which tend to be poorly crystalized. “Spinel-like” includes structures tend to approximate the spinel structure and also generally exhibit x-ray diffraction patterns typical of natural or synthetic spinels).

Examples of natural spinels suited for application according to the invention include MgAl₂O₄ (Spinel), MnAl₂O₄(Galaxite), FeAl₂O₄(Hercynite), ZnAl₂O₄ (Gahnite), MgFe₂O₄ (Magnesioferrite), MnFe₂O⁻ ₄ (Jacobsite), Fe₃O₄ (Magnetite), ZnFe₂O₄ (Franklinite), NiFe₂O₄ (Trevorite), CuFe₂O₄ (Cuprospinel), Fe₃S₄ (Greigite), MgCr₂O₄ (Magnesiochromite), (Mn,Fe)(Cr,V)₂O₄ (Manganochromite), FeCr₂O₄ (Chromite), (Ni,Fe)(Cr,V)₂O₄ (Nichromite), (Co,Ni)(Cr,Al)₂O₄ (Cochromite), MgV₂O₄ (Magnesiocoulsonite), FeV₂O₄ (Coulsonite), (Mn,Fe)(V,Cr)₂O₄ (Vuorelainenite), Mn₃O₄ (Hausmannite), CuCO₂S₄ (Carrolite), CuBi₂O₄ (Kusachiite), Mn(Mn,Fe)₂O₄ (Iwakiite) and ZnMn₂O₄ (Hataerolite).

For purposes of this invention, compounds having generally the AB₂X₄ formula A can include any of the following: Co²⁺, Cu²⁺, Fe²⁺, Mg²⁺, Mn²⁺, Ni²⁺ and Zn²⁺, and B can include any of the following: Al³⁺, Bi³⁺, Co³⁺, Cr³⁺, Fe³⁺, Mn³⁺ and V³⁺.

In demonstrating the present invention, it has been shown that adsorption of arsenic contaminants by mixed valency inorganic materials occurs largely independently of their degree of crystallization. For purposes of the present invention, it is recognized that the degree of crystallinity of, for example, spinel and spinel-like materials can vary from a slightly disordered amorphous material to a highly ordered material characterized by the face-centered cubic structures typically associated with natural spinels. This variability in crystallinity depends on factors such as particle size, exposure to heat, and time. Yet, according to the invention, so long as metal oxide and/or metal sulfide groups in a protonated state are in contact with the liquid containing the anionic contaminants, those anionic species can be successfully sorbed.

At any given pH, the extent of sorption is measured in terms of K_(d) (ml/g). This value represents the sorption coefficient, that is, the ratio of contaminant sorbed (moles/g) to contaminant in solution (moles/ml): Kd(ml/g)=[(Co−Ce)/Ce]×[Vsol(cc)/Mads(g)] where Co represents initial concentration, Ce represents final concentration, Vsol represents total volume of solution, and Mads represents total mass of adsorbent. Materials with Kd values greater than 100 ml/g are generally considered strong candidates for use as contaminant sorbents.

Without further elaboration, it is believed that one skilled in the art can, using the preceding description, utilize the present invention to its fullest extent. The following example of an embodiment is therefore intended to be construed as merely illustrative and not limitative of the remainder of the disclosure in any way whatsoever.

EXAMPLE

The following is an example showing synthesis, characterization and testing of MgAl₂O₄ for purposes of decontamination of arsenic-containing aqueous solutions.

Synthesis and Characterization: A 500 ml solution of 0.14M Mg(NO₃)₂.6H₂O (reagent grade) in deionized water was combined with a 500 ml solution of Al(NO₃)₃.9H₂O (reagent grade) in deionized water and mixed thoroughly using a magnetic stirrer. A solution of 3M NaOH (reagent grade) was added dropwise until the mixture reached a pH of approximately 9.0, at which point the Mg⁺² and Al⁺³ precipitated out of solution as mixed hydroxides. These precipitates were allowed to age for 24 hours at 298 K, and were then centrifuged and washed multiple times with deionized water to remove all NaNO₃ salts. The precipitates were then filtered with a Millipore pneumatic filter apparatus using a 0.45 μM filter and then mixed with 500 ml of pure ethanol (reagent grade). The resulting slurry was then allowed to dry in trays at ambient temperature and humidity. These powders were then divided into three groups (unheated), heated for 4 hours at 673 K in an oxidizing atmosphere, and heated for 4 hours at 1073 K in an oxidizing atmosphere. These powders were then characterized using X-ray diffraction. The results of these analyses are included in Table 1.

Testing: Batch sorption experiments were then performed to test the ability of MgAl₂O₄ to sorb arsenate (AsV) and chromate (Cr6). Solutions containing 100 ppb, 1 ppm, and 100 ppm of arsenate (or chromate) in a tap water matrix were synthesized. The analysis of the tap water is given in Table 2. In these experiments, 0.25 g of the unheated and heat-treated sorbents were mixed with 20 ml of the arsenic containing solutions for a contact time of 5 minutes. The solutions were then filtered using a 0.2 um filter and the resulting arsenic concentration was analyzed using inductively coupled plasma mass spectroscopy (ICP-MS). The results of these analysis and the calculated Kd's are presented in Table 3.

Similar synthesis was performed for a number of other compounds. Table 1 presents x-ray diffraction results showing phases resulting for various stoichiometries at different temperatures. Table 2 presents an analysis of the tap water matrix used prior to adding arsenic. This is instructive since it demonstrates, in conjunction with Table 3, that parts per billion levels of arsenic can be removed from water using the invention even where parts per million levels of other naturally occurring substances are present in the water. Table 3 presents sorption results for both arsenic and chromate.

TABLE 1 Unheated (298° C.) 400° C. 800° C. CoAl₂O₄ Al(OH)₃ + CoOOH CoAl₂O₄ (spinel) CoAl₂O₄ (spinel) CuAl₂O₄ CuAl₂O₄ (spinel-like) + CuO CuAl₂O₄ (spinel-like) + CuO CuAl₂O₄ (spinel) MgAl₂O₄ Al(OH)₃ + Mg(OH)₂ MgAl₂O₄ (spinel-like) MgAl₂O₄ (spinel) NiAl₂O₄ Al(OH)₃ + NiOOH NiAl₂O₄ (spinel-like) NiAl₂O₄ (spinel) ZnAl₂O₄ Zn₆Al₂(OH)₁₆CO₃•4H₂O + Al(OH)₃ ZnAl₂O₄ (spinel-like) ZnAl₂O₄ (spinel) CuCr₂O₄ Cu₃CrO₆•2H₂O + Cr(OH)₃ CuCr₂O₄ (spinel-like) + Cr₂O₃ CuCr₂O₄ (spinel-like) + Cr₂O₃ CuFe₂O₄ CuFe₂O₄ (spinel-like) CuFe₂O₄ (spinel) + CuO + Fe₂O₃ CuFe₂O₄ (spinel) MgFe₂O₄ MgFe₂O₄ (spinel-like) MgFe₂O₄ (spinel) MgFe₂O₄ (spinel) ZnFe₂O₄ ZnFe₂O₄ (spinel-like) ZnFe₂O₄ (spinel) ZnFe₂O₄ (spinel)

TABLE 2 (General Chemistry Analysis of Tap Water Matrix) pH 7.7 Chloride 33 ppm Silica 40 ppm as SiO₂ Sulfate 26 ppm Fluoride 1 ppm Bicarbonate 106 ppm as CaCO₃

TABLE 3 ARSENIC SORPTION Arsenic Arsenic Init. Final Material Conc (ppb) Conc. (ppb) Kd (ml/g) CoAl₂O₄ (spinel-800 C.) 132 2 5200 CuAl₂O₄ (spinel-like-400 C.) 132 <0.2 52720 CuAl₂O₄ (spinel-800 C.) 132 1.9 5478 MgAl₂O₄ (spinel-like-400 C.) 192 5 2992 MgAl₂O₄ (spinel-800 C.) 192 16 880 NiAl₂O₄ (spinel-like-400 C.) 132 <0.2 52720 NiAl₂O₄ (spinel-800 C.) 132 2.6 3982 ZnAl₂O₄ (spinel-like-400 C.) 132 <0.2 52720 ZnAl₂O₄ (spinel-800 C.) 132 0.7 15006 Co₃O₄ (spinel-400 C.) 132 4.5 2267 CuFe₂O₄ (spinel-like-unheated) 132 0.4 26320 CuFe₂O₄ (spinel-400 C.) 132 13 732 MgFe₂O₄ (spinel-like-unheated) 132 0.72 14587 MgFe₂O₄ (spinel-400 C.) 132 1.2 8720 ZnFe₂O₄ (spinel-like-unheated) 132 0.9 11653 ZnFe₂O₄ (spinel-400 C.) 132 6.7 1496 CHROMATE SORPTION Cr Init. Cr Final Material Conc (ppb) Conc. (ppb) Kd (ml/g) CoAl₂O₄ (spinel-800 C.) 1010 3 26853 CuAl₂O₄ (spinel-800 C.) 1010 81 916 MgAl₂O₄ (spinel-like-400 C.) 1010 122 582 NiAl₂O₄ (spinel-like-400 C.) 1010 3 26853 NiAl₂O₄ (spinel-800 C.) 1010 104 697 ZnAl₂O₄ (spinel-like-400 C.) 1010 3 26853 CuFe₂O₄ (spinel-like-unheated) 1010 40 1940 MgFe₂O₄ (spinel-like-unheated) 1010 39 1992 MgFe₂O₄ (spinel-400 C.) 1010 31 2526

From the foregoing description, one skilled in the art can easily a certain the essential characteristics of the invention defined in this specification and the appended claims, and without departing from the spirit and scope thereof can make various changes and modifications of the invention to adapt it to various usages and conditions. Such changes and modifications as would be obvious to one skilled in the art are intended to be included within the scope of the following claims. Additional advantages and novel features will become apparent to those skilled in the art upon examination of the following description or may be learned by practice of the invention. 

1. A water decontamination process comprising: selecting sorbent material that binds anionic species predominantly through the formation of surface complexes, said sorbent material comprising a composition including formula (AB₂X₄)_(n) wherein A is a divalent cation selected from the group consisting of Co²⁺, Cu²⁺, Ni²⁺, Zn²⁺, B is a trivalent cation selected from the group consisting of Al³⁺, Bi³⁺, Co³⁺, Cr³⁺, Fe³⁺, Mn³⁺, Ni³⁺, and V³⁺, X is an anion species selected from the group consisting of oxygen and sulfur, n is at least one, and decontaminating water by contacting said selected sorbent material with water containing anionic contaminants, the anionic contaminants selected from the group consisting of species including chromium and species including arsenic, said decontaminating substantially removing the anionic contaminants.
 2. The process of claim 1, wherein the anionic contaminants consist of species including arsenic.
 3. The process of claim 1, wherein the anionic contaminants consist of species including chromium.
 4. The process of claim 1 wherein said sorbent material is selected from the group consisting of ZnAl₂O₄, ZnFe₂O₄, NiFe₂O₄, CuAl₂O₄, CuFe₂O₄, (Ni,)(Cr,V)₂O₄, (Co,Ni)(Cr,Al)₂O₄, CuCo₂S₄, CuBi₂O₄, and ZnMn₂O₄.
 5. A process for decontaminating water, comprising: selecting a sorbent material that binds anionic species predominantly through the formation of surface complexes, said sorbent material having a formula (AB₂X₄)_(n), wherein: n is at least one; A is an element selected from the group consisting of Co²⁺, Cu²⁺, Fe²⁺, Mn²⁺, Ni²⁺, and Zn²⁺; B is an element selected from the group consisting of Al³⁺, Bi³⁺, Co³⁺, Cr³⁺, Fe³⁺, Mn³⁺, Ni³⁺, and V³⁺; X is selected from oxygen and sulfur, wherein B is a different element than A; and decontaminating water of arsenic contaminants by contacting said selected sorbent material with water containing anionic contaminants, the anionic contaminants being from the group consisting of species including chromium and species including arsenic, said decontaminating substantially removing the anionic contaminants.
 6. The process of claim 5, wherein the anionic contaminants consist of species including arsenic.
 7. The process of claim 5, wherein the anionic contaminants consist of species including chromium.
 8. The process of claim 5 wherein said sorbent material comprises a chemical substance selected from the group consisting of MnAl₂O₄, FeAl₂O₄, ZnAl₂O₄, MnFe₂O₄, ZnFe₂O₄, NiFe₂O₄, CuFe₂O₄, CuAl₂O₄, (Mn,Fe)(Cr,V)₂O₄, FeCr₂O₄, (Ni,Fe)(Cr,V)₂O₄, (Co,Ni)(Cr,Al)₂O₄, FeV₂O₄, Fe₂TiO₄, CuCO₂O₄, CuBi₂O₄, and ZnMn₂O₄.
 9. The process of claim 5, wherein said selected sorbent material is CuAl₂O₄.
 10. A process for decontaminating water, comprising: selecting a sorbent material that binds anionic species predominantly through the formation of surface complexes, said sorbent selected from the group consisting of MgFe₂O₄, MnFe₂O₄, ZnFe₂O₄, NiFe₂O₄, CuAl₂O₄, CuFe₂O₄, MgCr₂O₄, MnCr₂O₄ FeCr₂O₄, NiCr₂O₄, CoCr₂O₄, MgV₂O₄, MnV₂O₄, FeV₂O₄, NiV₂O₄, Mg₂TiO₄, Fe₂TiO₄, CuCO₂O₄, CuBi₂O₄, MnAl₂O₄ and ZnMn₂O₄, decontaminating water of contaminants by contacting said selected sorbent material with water containing anionic contaminants, the anionic contaminants being from the group consisting of species including chromium and species including arsenic, said decontaminating substantially removing the anionic contaminants.
 11. The process of claim 10, wherein the anionic contaminates consist of species including arsenic.
 12. The process of claim 10, wherein said selected sorbent material is CuAl₂O₄. 